Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2570 | KDB | |
PAff | 782.50 | kJ/mol | NIST |
Tig | 729.26 | K | KDB |
BasG | 751.50 | kJ/mol | NIST |
ΔcH°liquid | -972.61 ± 0.59 | kJ/mol | NIST |
μ | 1.80 | debye | KDB |
η | 0.0003000 | Pa×s | Densiti... |
LFL | 5.00 | % in Air | KDB |
UFL | 22.70 | % in Air | KDB |
Tflash,oc | 240.93 | K | KDB |
ΔfG° | -297.40 | kJ/mol | KDB |
ΔfH°gas | [-362.00; -336.90] | kJ/mol | |
ΔfH°gas | -350.00 | kJ/mol | KDB |
ΔfH°gas | -336.90 | kJ/mol | NIST |
ΔfH°gas | -349.00 | kJ/mol | NIST |
ΔfH°gas | -362.00 | kJ/mol | NIST |
ΔfH°gas | -355.50 | kJ/mol | NIST |
ΔfH°liquid | [-391.00; -365.90] | kJ/mol | |
ΔfH°liquid | -365.90 | kJ/mol | NIST |
ΔfH°liquid | -378.00 | kJ/mol | NIST |
ΔfH°liquid | -391.00 | kJ/mol | NIST |
ΔfH°liquid | -386.10 | kJ/mol | NIST |
ΔfusH° | 4.41 | kJ/mol | Joback Calculated Property |
ΔvapH° | 29.18 | kJ/mol | Joback Calculated Property |
IE | [10.30; 11.00] | eV | |
IE | 10.84 | eV | NIST |
IE | 10.84 | eV | NIST |
IE | 10.70 | eV | NIST |
IE | 10.99 | eV | NIST |
IE | 10.85 ± 0.05 | eV | NIST |
IE | 10.85 | eV | NIST |
IE | 10.81 ± 0.01 | eV | NIST |
IE | 11.00 | eV | NIST |
IE | 10.85 | eV | NIST |
IE | Outlier 10.30 | eV | NIST |
log10WS | [0.58; 0.58] | ||
log10WS | 0.58 | Aq. Sol... | |
log10WS | 0.58 | Estimat... | |
logPoct/wat | -0.211 | Crippen Calculated Property | |
McVol | 46.480 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 1 | KDB | |
Pc | [5998.00; 6247.00] | kPa | |
Pc | 5998.00 | kPa | KDB |
Pc | 6004.00 ± 60.79 | kPa | NIST |
Pc | 6007.50 ± 40.00 | kPa | NIST |
Pc | 6247.00 ± 202.65 | kPa | NIST |
ρc | [349.38; 349.38] | kg/m3 | |
ρc | 349.38 ± 4.80 | kg/m3 | NIST |
ρc | 349.38 ± 4.20 | kg/m3 | NIST |
Inp | [362.00; 407.00] | ||
Inp | 376.00 | NIST | |
Inp | 377.00 | NIST | |
Inp | 369.00 | NIST | |
Inp | 369.00 | NIST | |
Inp | 373.00 | NIST | |
Inp | 370.00 | NIST | |
Inp | 386.00 | NIST | |
Inp | 373.00 | NIST | |
Inp | 380.00 | NIST | |
Inp | 362.00 | NIST | |
Inp | 370.00 | NIST | |
Inp | 386.00 | NIST | |
Inp | 401.10 | NIST | |
Inp | 386.00 | NIST | |
Inp | 386.00 | NIST | |
Inp | 407.00 | NIST | |
Inp | 407.00 | NIST | |
Inp | 401.10 | NIST | |
I | [757.00; 779.00] | ||
I | 779.00 | NIST | |
I | 757.00 | NIST | |
I | 779.00 | NIST | |
I | 761.00 | NIST | |
I | 779.00 | NIST | |
Tboil | [304.70; 304.89] | K | |
Tboil | 304.80 | K | KDB |
Tboil | 304.70 | K | Solutio... |
Tboil | 304.79 | K | Isobari... |
Tboil | 304.70 | K | Isobari... |
Tboil | 304.89 | K | Isobari... |
Tc | [485.20; 523.70] | K | |
Tc | 487.20 | K | KDB |
Tc | 487.20 | K | NIST |
Tc | 487.20 ± 1.00 | K | NIST |
Tc | 487.20 ± 1.00 | K | NIST |
Tc | Outlier 523.70 ± 20.00 | K | NIST |
Tc | 485.20 ± 2.00 | K | NIST |
Tfus | [173.20; 174.00] | K | |
Tfus | 174.00 | K | KDB |
Tfus | 173.40 | K | Aq. Sol... |
Tfus | 173.20 ± 2.00 | K | NIST |
Tfus | 173.40 ± 0.30 | K | NIST |
Vc | 0.172 | m3/kmol | KDB |
Zc | 0.2546780 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [73.11; 92.17] | J/mol×K | [316.24; 489.79] | |
Cp,gas | 73.11 | J/mol×K | 316.24 | Joback Calculated Property |
Cp,gas | 76.36 | J/mol×K | 345.17 | Joback Calculated Property |
Cp,gas | 79.59 | J/mol×K | 374.09 | Joback Calculated Property |
Cp,gas | 82.80 | J/mol×K | 403.02 | Joback Calculated Property |
Cp,gas | 85.96 | J/mol×K | 431.94 | Joback Calculated Property |
Cp,gas | 89.09 | J/mol×K | 460.87 | Joback Calculated Property |
Cp,gas | 92.17 | J/mol×K | 489.79 | Joback Calculated Property |
Cp,liquid | [95.50; 130.00] | J/mol×K | [288.00; 298.75] | |
Cp,liquid | 121.30 | J/mol×K | 288.00 | NIST |
Cp,liquid | 95.50 | J/mol×K | 297.00 | NIST |
Cp,liquid | 130.00 | J/mol×K | 298.00 | NIST |
Cp,liquid | 119.70 | J/mol×K | 298.15 | NIST |
Cp,liquid | 120.57 | J/mol×K | 298.75 | NIST |
η | [0.0002358; 0.0018060] | Pa×s | [176.53; 316.24] | |
η | 0.0018060 | Pa×s | 176.53 | Joback Calculated Property |
η | 0.0010556 | Pa×s | 199.81 | Joback Calculated Property |
η | 0.0006902 | Pa×s | 223.10 | Joback Calculated Property |
η | 0.0004890 | Pa×s | 246.38 | Joback Calculated Property |
η | 0.0003677 | Pa×s | 269.67 | Joback Calculated Property |
η | 0.0002893 | Pa×s | 292.95 | Joback Calculated Property |
η | 0.0002358 | Pa×s | 316.24 | Joback Calculated Property |
ΔvapH | [27.40; 30.10] | kJ/mol | [283.00; 374.00] | |
ΔvapH | 30.10 | kJ/mol | 283.00 | NIST |
ΔvapH | 29.60 | kJ/mol | 292.00 | NIST |
ΔvapH | 28.70 ± 0.10 | kJ/mol | 293.00 | NIST |
ΔvapH | 27.92 | kJ/mol | 304.70 | NIST |
ΔvapH | 27.90 ± 0.10 | kJ/mol | 305.00 | NIST |
ΔvapH | 28.20 | kJ/mol | 305.10 | KDB |
ΔvapH | 27.40 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 28.40 | kJ/mol | 374.00 | NIST |
Pvap | [101.32; 114.88] | kPa | [304.70; 308.15] | |
Pvap | 101.32 | kPa | 304.70 | Isobari... |
Pvap | 114.88 | kPa | 308.15 | Total V... |
n0 | [1.33930; 1.34359] | [293.10; 303.15] | ||
n0 | 1.34359 | 293.10 | Vapor-L... | |
n0 | 1.34150 | 298.15 | Thermod... | |
n0 | 1.34110 | 298.15 | Mixing ... | |
n0 | 1.34020 | 299.15 | Excess ... | |
n0 | 1.33930 | 303.15 | Excess ... | |
ρl | [960.85; 980.82] | kg/m3 | [288.15; 298.15] | |
ρl | 980.82 | kg/m3 | 288.15 | Isobari... |
ρl | 977.21 | kg/m3 | 291.15 | Experim... |
ρl | 974.00 | kg/m3 | 293.00 | KDB |
ρl | 966.54 | kg/m3 | 298.15 | Experim... |
ρl | 960.85 | kg/m3 | 298.15 | Densiti... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 4511.72] | kPa | [224.24; 487.20] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42260e+01 | |||
Coefficient B | -2.62106e+03 | |||
Coefficient C | -3.61910e+01 | |||
Temperature range, min. | 224.24 | |||
Temperature range, max. | 487.20 | |||
Pvap | 1.33 | kPa | 224.24 | Calculated Property |
Pvap | 8.69 | kPa | 253.46 | Calculated Property |
Pvap | 36.31 | kPa | 282.68 | Calculated Property |
Pvap | 112.07 | kPa | 311.89 | Calculated Property |
Pvap | 278.69 | kPa | 341.11 | Calculated Property |
Pvap | 590.95 | kPa | 370.33 | Calculated Property |
Pvap | 1110.43 | kPa | 399.55 | Calculated Property |
Pvap | 1899.55 | kPa | 428.76 | Calculated Property |
Pvap | 3016.54 | kPa | 457.98 | Calculated Property |
Pvap | 4511.72 | kPa | 487.20 | Calculated Property |
Pvap | [7.18e-03; 5921.32] | kPa | [174.15; 487.20] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.57116e+01 | |||
Coefficient B | -5.45175e+03 | |||
Coefficient C | -7.66441e+00 | |||
Coefficient D | 6.72918e-06 | |||
Temperature range, min. | 174.15 | |||
Temperature range, max. | 487.20 | |||
Pvap | 7.18e-03 | kPa | 174.15 | Calculated Property |
Pvap | 0.36 | kPa | 208.93 | Calculated Property |
Pvap | 5.04 | kPa | 243.72 | Calculated Property |
Pvap | 33.51 | kPa | 278.50 | Calculated Property |
Pvap | 137.25 | kPa | 313.28 | Calculated Property |
Pvap | 406.95 | kPa | 348.07 | Calculated Property |
Pvap | 965.64 | kPa | 382.85 | Calculated Property |
Pvap | 1957.94 | kPa | 417.63 | Calculated Property |
Pvap | 3546.70 | kPa | 452.42 | Calculated Property |
Pvap | 5921.32 | kPa | 487.20 | Calculated Property |
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